2013Journal of Dispersion Science and TechnologyRequires access

Separation and Extraction of Uranium from Leach Liquor Containing Uranium and Molybdenum by Solvent Extraction with LIX 622N

M. E. Ibrahim, T.A. Lasheen, H.B. Hassib, Ahmed Helal

Open publisher page 15 citations

Abstract

The leach liquor (0.5 g/L Mo, 0.05 g/L U) obtained from the leaching process of molybdenum-uranium ore material was treated using solvent extraction to recover U(VI) by LIX 622N, which is a salicylaldoxime derivative. The influence of various basic variables such as pH, concentration of LIX 622N, temperature, different stripping reagents, phase ratio, and diluents was examined. Using 10% LIX 622N with the aqueous solution of equilibrium pH 6.0 and a phase ratio organic phase:aqueous phase (O:A) = 1:1, a two-stage McCabe-Thiele plot was constructed, which showed 99.9% of U extraction with no co-extraction of molybdenum. This was confirmed by a 6-cycle counter current simulation (CCS) study. The obtained data of temperature on the extraction of uranium showed that the extraction process is exothermic with enthalpy change of −20.949 kJ mol−1. The stripping of U(VI) was quantitative using 4 M H2SO4. The stable complex UO2(HSO4)Rorg formed during extraction, which supports the cation exchange mechanism, and was confirmed by FTIR spectral analysis.

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What this paper is about

The leach liquor (0.5 g/L Mo, 0.05 g/L U) obtained from the leaching process of molybdenum-uranium ore material was treated using solvent extraction to recover U(VI) by LIX 622N, which is a salicylaldoxime derivative. The influence of various basic variables such as pH, concentration of LIX 622N, temperature, different stripping reagents, phase ratio, and diluents was examined. Using 10% LIX 622N with the aqueous solution of equilibrium pH 6.0 and a phase ratio organic phase:aqueous phase (O:A) = 1:1, a two-stage McCabe-Thiele plot was constructed, which showed 99.9% of U extraction with no co-extraction of molybdenum. This was confirmed by a 6-cycle counter current simulation (CCS) study. The obtained data of temperature on the extraction of uranium showed that the extraction process is exothermic with enthalpy change of −20.949 kJ mol−1. The stripping of U(VI) was quantitative using 4 M H2SO4. The stable complex UO2(HSO4)Rorg formed during extraction, which supports the cation exchange mechanism, and was confirmed by FTIR spectral analysis.

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Available abstract

The leach liquor (0.5 g/L Mo, 0.05 g/L U) obtained from the leaching process of molybdenum-uranium ore material was treated using solvent extraction to recover U(VI) by LIX 622N, which is a salicylaldoxime derivative. The influence of various basic variables such as pH, concentration of LIX 622N, temperature, different stripping reagents, phase ratio, and diluents was examined. Using 10% LIX 622N with the aqueous solution of equilibrium pH 6.0 and a phase ratio organic phase:aqueous phase (O:A) = 1:1, a two-stage McCabe-Thiele plot was constructed, which showed 99.9% of U extraction with no co-extraction of molybdenum. This was confirmed by a 6-cycle counter current simulation (CCS) study. The obtained data of temperature on the extraction of uranium showed that the extraction process is exothermic with enthalpy change of −20.949 kJ mol−1. The stripping of U(VI) was quantitative using 4 M H2SO4. The stable complex UO2(HSO4)Rorg formed during extraction, which supports the cation exchange mechanism, and was confirmed by FTIR spectral analysis.

Key concepts: Chemistry, Molybdenum, Uranium, Extraction (chemistry), Stripping (fiber), Diluent, Aqueous two-phase system, Aqueous solution

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Separation and Extraction of Uranium from Leach Liquor Containing Uranium and Molybdenum by Solvent Extraction with LIX 622N — Research Paper | ScholarLens